NO20051952L - Method and system for separating a component from a multi-component gas - Google Patents
Method and system for separating a component from a multi-component gasInfo
- Publication number
- NO20051952L NO20051952L NO20051952A NO20051952A NO20051952L NO 20051952 L NO20051952 L NO 20051952L NO 20051952 A NO20051952 A NO 20051952A NO 20051952 A NO20051952 A NO 20051952A NO 20051952 L NO20051952 L NO 20051952L
- Authority
- NO
- Norway
- Prior art keywords
- component
- gas
- velocity
- separating
- flow line
- Prior art date
Links
- 238000000034 method Methods 0.000 title abstract 2
- 239000012466 permeate Substances 0.000 abstract 3
- 239000000203 mixture Substances 0.000 abstract 1
- 238000010926 purge Methods 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/06—Tubular membrane modules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/04—Tubular membranes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/144—Purification; Separation; Use of additives using membranes, e.g. selective permeation
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
- C10L3/101—Removal of contaminants
- C10L3/102—Removal of contaminants of acid contaminants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/504—Carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/22—Cooling or heating elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/22—Cooling or heating elements
- B01D2313/221—Heat exchangers
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2
Abstract
En fremgangsmåte og apparatur for å separere en komponent fra en flerkomponent tilførselsgasstrøm har en strømningsledning (14) som har en semipermeabel seksjon (15) som slipper gjennom komponenten som skal separeres fra tilførselsgasstrømmen (12). En spylegass er tilveiebrakt ved en første hastighet på permeatsiden av strømningsledning (14) og hastigheten av spylegass (13) akselereres slik at hastigheten av spylegass (13) langs minst en del av permeatsiden av strømningsledning (14) er større enn den første hastigheten. Blandingen av permeat og spylegass (13) blir deretter bremset av diffusor (20), og gjenvinner derved som trykk en del av energien i tilførselsgasstrøm (12).A method and apparatus for separating a component from a multi-component feed gas stream has a flow line (14) having a semipermeable section (15) which passes through the component to be separated from the feed gas stream (12). A flush gas is provided at a first velocity on the permeate side of the flow line (14) and the velocity of the flush gas (13) is accelerated such that the velocity of the flush gas (13) along at least a portion of the permeate side of the flow line (14) is greater than the first velocity. The mixture of permeate and purge gas (13) is then slowed down by the diffuser (20), thereby recovering as pressure part of the energy in the supply gas stream (12).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US41335002P | 2002-09-25 | 2002-09-25 | |
PCT/US2003/020625 WO2004028665A1 (en) | 2002-09-25 | 2003-06-30 | Method and system for separating a component from a multi-component gas |
Publications (2)
Publication Number | Publication Date |
---|---|
NO20051952D0 NO20051952D0 (en) | 2005-04-21 |
NO20051952L true NO20051952L (en) | 2005-06-27 |
Family
ID=32043239
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO20051952A NO20051952L (en) | 2002-09-25 | 2005-04-21 | Method and system for separating a component from a multi-component gas |
Country Status (7)
Country | Link |
---|---|
US (1) | US7314502B2 (en) |
EP (1) | EP1549415A4 (en) |
AU (1) | AU2003299081A1 (en) |
CA (1) | CA2497317A1 (en) |
MX (1) | MXPA05003145A (en) |
NO (1) | NO20051952L (en) |
WO (1) | WO2004028665A1 (en) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8940265B2 (en) * | 2009-02-17 | 2015-01-27 | Mcalister Technologies, Llc | Sustainable economic development through integrated production of renewable energy, materials resources, and nutrient regimes |
US7972415B2 (en) * | 2008-12-11 | 2011-07-05 | Spx Corporation | Membrane-based compressed air breathing system |
US9097152B2 (en) * | 2009-02-17 | 2015-08-04 | Mcalister Technologies, Llc | Energy system for dwelling support |
US8808529B2 (en) * | 2009-02-17 | 2014-08-19 | Mcalister Technologies, Llc | Systems and methods for sustainable economic development through integrated full spectrum production of renewable material resources using solar thermal |
US9231267B2 (en) * | 2009-02-17 | 2016-01-05 | Mcalister Technologies, Llc | Systems and methods for sustainable economic development through integrated full spectrum production of renewable energy |
US20150086904A1 (en) * | 2009-02-17 | 2015-03-26 | Mcalister Technologies, Llc | Delivery systems with in-line selective extraction devices and associated methods of operation |
US20130240369A1 (en) * | 2009-02-17 | 2013-09-19 | Mcalister Technologies, Llc | Systems and methods for sustainable economic development through integrated full spectrum production of renewable energy |
US8814983B2 (en) | 2009-02-17 | 2014-08-26 | Mcalister Technologies, Llc | Delivery systems with in-line selective extraction devices and associated methods of operation |
US8313556B2 (en) * | 2009-02-17 | 2012-11-20 | Mcalister Technologies, Llc | Delivery systems with in-line selective extraction devices and associated methods of operation |
EP2533872A4 (en) * | 2010-02-13 | 2014-01-22 | Mcalister Technologies Llc | Delivery systems with in- line selective extraction devices and associated methods of operation |
ES2645988T3 (en) * | 2012-06-15 | 2017-12-11 | University Of Pittsburgh - Of The Commonwealth System Of Higher Education | Systems to reduce the concentration of carbon dioxide in the blood |
US10173389B2 (en) * | 2015-12-15 | 2019-01-08 | Bloom Energy Corporation | Carbon dioxide shielded natural gas line and method of using thereof |
EP3528880B1 (en) | 2016-10-19 | 2021-07-07 | Teleflex Medical Incorporated | Moisture removal and condensation and humidity management apparatus for a breathing circuit |
US10960165B2 (en) | 2017-07-10 | 2021-03-30 | Teleflex Medical Incorporated | Moisture removal and condensation and humidity management apparatus for a breathing circuit |
US11478745B2 (en) * | 2019-09-03 | 2022-10-25 | Arizona Board Of Regents On Behalf Of Arizona State University | Device and method for CO2 capture through circumscribed hollow membranes |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3735558A (en) * | 1971-06-29 | 1973-05-29 | Perma Pure Process Inc | Process for separating fluids and apparatus |
US3832830A (en) * | 1972-09-18 | 1974-09-03 | Du Pont | Permeation separation device |
US4031012A (en) | 1975-09-17 | 1977-06-21 | Gics Pharmaceuticals, Inc. | Separatory apparatus |
US4019868A (en) | 1976-03-24 | 1977-04-26 | The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration | Solar hydrogen generator |
US4666469A (en) * | 1985-05-29 | 1987-05-19 | The Dow Chemical Company | Hollow fiber membrane device with inner wrap |
US5013437A (en) * | 1989-10-30 | 1991-05-07 | The Dow Chemical Company | Hollow fiber membrane fluid separation device adapted for boreside feed which contains multiple concentric stages |
FR2663625B1 (en) | 1990-06-25 | 1992-09-11 | Air Liquide | PROCESS AND PLANT FOR PRODUCING PURE HYDROGEN. |
US5084073A (en) * | 1990-10-11 | 1992-01-28 | Union Carbide Industrial Gases Technology Corporation | Membrane drying process and system |
US5183486A (en) | 1990-12-04 | 1993-02-02 | Spectra-Physics, Inc. | Apparatus for degassing a liquid |
US5820654A (en) * | 1997-04-29 | 1998-10-13 | Praxair Technology, Inc. | Integrated solid electrolyte ionic conductor separator-cooler |
US6280502B1 (en) * | 1998-12-31 | 2001-08-28 | Shell Oil Company | Removing solids from a fluid |
GC0000091A (en) | 1998-12-31 | 2004-06-30 | Shell Int Research | Method for removing condensables from a natural gas stream. |
JP3816289B2 (en) * | 2000-02-18 | 2006-08-30 | ナブテスコ株式会社 | Hollow fiber membrane dehumidifier |
US6293084B1 (en) | 2000-05-04 | 2001-09-25 | Praxair Technology, Inc. | Oxygen separator designed to be integrated with a gas turbine and method of separating oxygen |
US6558450B2 (en) * | 2001-03-22 | 2003-05-06 | Celgard Inc. | Method for debubbling an ink |
US20050092683A1 (en) * | 2003-10-31 | 2005-05-05 | Goldsmith Robert L. | Membrane devices for pervaporation, gas separations, and perstraction with permeate and sweep fluid conduit and method of use |
-
2003
- 2003-06-30 EP EP03742349A patent/EP1549415A4/en not_active Withdrawn
- 2003-06-30 US US10/526,099 patent/US7314502B2/en not_active Expired - Fee Related
- 2003-06-30 AU AU2003299081A patent/AU2003299081A1/en not_active Abandoned
- 2003-06-30 WO PCT/US2003/020625 patent/WO2004028665A1/en not_active Application Discontinuation
- 2003-06-30 CA CA002497317A patent/CA2497317A1/en not_active Abandoned
- 2003-06-30 MX MXPA05003145A patent/MXPA05003145A/en active IP Right Grant
-
2005
- 2005-04-21 NO NO20051952A patent/NO20051952L/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
EP1549415A4 (en) | 2007-03-14 |
EP1549415A1 (en) | 2005-07-06 |
WO2004028665A1 (en) | 2004-04-08 |
NO20051952D0 (en) | 2005-04-21 |
US20060162554A1 (en) | 2006-07-27 |
MXPA05003145A (en) | 2005-06-22 |
US7314502B2 (en) | 2008-01-01 |
AU2003299081A1 (en) | 2004-04-19 |
CA2497317A1 (en) | 2004-04-08 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FC2A | Withdrawal, rejection or dismissal of laid open patent application |